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公开(公告)号：US20140252276A1
公开(公告)日：2014-09-11
申请号：US14347431
申请日：2012-09-27
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
CPC classification number: C01B3/52 , B01D5/0027 , B01D5/006 , B01D5/0072 , B01D5/0075 , B01D5/009 , B01D17/0208 , B01D29/27 , B01D29/66 , B01D46/0036 , B01D47/10 , B01D50/006 , B01D53/0423 , B01D53/0462 , B01D53/047 , B01D53/0476 , B01D53/12 , B01D53/1406 , B01D53/1412 , B01D53/1431 , B01D53/1462 , B01D53/1468 , B01D53/1487 , B01D53/18 , B01D53/265 , B01D53/326 , B01D53/48 , B01D53/76 , B01D61/362 , B01D2252/102 , B01D2252/103 , B01D2252/20436 , B01D2252/504 , B01D2252/602 , B01D2256/16 , B01D2256/20 , B01D2257/304 , B01D2257/306 , B01D2257/406 , B01D2257/504 , B01D2257/60 , B01D2257/708 , B01D2259/402 , C01B3/24 , C01B3/38 , C01B3/382 , C01B3/386 , C01B3/56 , C01B3/58 , C01B2203/0227 , C01B2203/0233 , C01B2203/025 , C01B2203/0261 , C01B2203/04 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0435 , C01B2203/045 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/0877 , C01B2203/1235 , C01B2203/1241 , C01B2203/142 , C01B2203/147 , C01B2203/84 , H05K999/99 , Y02P20/13 , Y02P30/30
Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.
Abstract translation: 用于处理未条件合成气的系统和方法首先除去固体和半挥发性有机化合物（SVOC），然后除去挥发性有机化合物（VOC），然后从合成气中除去至少一种含硫化合物。 可以根据诸如待处理的合成气的来源，期望形成，捕获或再循环的产物，副产物和中间产物等因素进行附加处理和环境考虑。
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公开(公告)号：US20250059036A1
公开(公告)日：2025-02-20
申请号：US18821604
申请日：2024-08-30
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
IPC: C01B3/52 , B01D5/00 , B01D17/02 , B01D29/27 , B01D29/66 , B01D46/00 , B01D47/10 , B01D50/60 , B01D53/04 , B01D53/047 , B01D53/12 , B01D53/14 , B01D53/18 , B01D53/26 , B01D53/32 , B01D53/48 , B01D53/76 , B01D61/36 , C01B3/24 , C01B3/38 , C01B3/56 , C01B3/58
Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.
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13.发明授权公开(公告)号：US12187969B2
公开(公告)日：2025-01-07
申请号：US18151095
申请日：2023-01-06
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Dave G. Newport , Daniel A. Burciaga , Daniel Michael Leo , Justin Kevin Miller , Brian Christopher Attwood
IPC: C01B3/34 , B01J19/00 , B01J19/24 , C01B3/50 , C07C29/151 , C07C41/01 , C10G2/00 , C10J3/84 , C10K1/00 , C10K3/06 , C10L1/02 , C10L1/06 , C10L1/08 , C12P7/06
Abstract: A method of producing liquid fuel and/or chemicals from a carbonaceous material entails combusting a conditioned syngas in pulse combustion heat exchangers of a steam reformer to help convert carbonaceous material into first reactor product gas which includes carbon monoxide, hydrogen, carbon dioxide and other gases. A portion of the first reactor product gas is transferred to a hydrogen reformer into which additional conditioned syngas is added and a reaction carried out to produce an improved syngas. The improved syngas is then subject to one or more gas clean-up steps to form a new conditioned syngas. A portion of the new conditioned syngas is recycled to be used as the conditioned syngas in the pulse combustion heat exchangers and in the hydrocarbon reformer. A system for carrying out the method include, a steam reformer, a hydrocarbon reformer, first and second gas-cleanup systems, a synthesis system and an upgrading system.
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公开(公告)号：US20230391618A1
公开(公告)日：2023-12-07
申请号：US18233028
申请日：2023-08-11
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
IPC: C01B3/52 , C01B3/56 , B01D50/60 , B01D53/047 , B01D53/12 , B01D53/14 , B01D53/18 , B01D53/32 , C01B3/24 , B01D5/00 , B01D47/10 , B01D17/02 , B01D29/27 , B01D29/66 , B01D46/00 , B01D53/04 , B01D53/48 , B01D53/76 , B01D61/36 , C01B3/38 , C01B3/58 , B01D53/26
CPC classification number: C01B3/52 , C01B3/56 , B01D50/60 , B01D53/047 , B01D53/12 , B01D53/1406 , B01D53/1462 , B01D53/1487 , B01D53/18 , B01D53/326 , C01B3/24 , B01D5/006 , B01D5/0072 , B01D5/0075 , B01D47/10 , B01D17/0208 , B01D29/27 , B01D29/66 , B01D5/0027 , B01D5/009 , B01D46/0036 , B01D53/0423 , B01D53/0462 , B01D53/0476 , B01D53/1412 , B01D53/1431 , B01D53/1468 , B01D53/48 , B01D53/76 , B01D61/362 , C01B3/38 , C01B3/382 , C01B3/386 , C01B3/58 , B01D53/265 , H05K999/99 , C01B2203/0233 , C01B2203/0415 , C01B2203/043 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , Y02P20/129 , Y02P30/00 , B01D2252/103 , B01D2252/504 , B01D2257/708 , B01D2259/402 , C01B2203/042 , B01D2252/102 , B01D2252/20436 , B01D2252/602 , B01D2256/16 , B01D2256/20 , B01D2257/304 , B01D2257/306 , B01D2257/406 , B01D2257/504 , B01D2257/60 , C01B2203/0227 , C01B2203/025 , C01B2203/04 , C01B2203/045 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/0877 , C01B2203/84 , C01B2203/0261 , C01B2203/0435 , C01B2203/1235 , C01B2203/1241 , C01B2203/142 , C01B2203/147
Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.
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15.发明授权公开(公告)号：US11760949B2
公开(公告)日：2023-09-19
申请号：US17957670
申请日：2022-09-30
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Dave G. Newport , Daniel A. Burciaga , Daniel Michael Leo
CPC classification number: C10J3/721 , C10K1/005 , C10K1/026 , C10J2300/0946 , C10J2300/0959 , C10J2300/1261 , C10J2300/1618 , C10J2300/1637 , C10J2300/1815 , C10J2300/1846 , C10J2300/1853
Abstract: A two-stage syngas production method to produce a final product gas from a carbonaceous material includes producing a first product gas in a first reactor, separating char from the first product gas to produce separated char and char-depleted product gas, and separately reacting the separated char and the char-depleted product gas with an oxygen-containing gas in a second reactor to produce a final product gas. The separated char is introduced into the second reactor above the char-depleted product gas. The solids separation device may include serially connected cyclones, and the separated char may be entrained in a motive fluid in an eductor to produce a char and motive fluid mixture prior to being transferred to the second reactor. A biorefinery method produces a purified product from the final product gas.
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Patent Agency Ranking
公开(公告)号：US11760631B2
公开(公告)日：2023-09-19
申请号：US17534251
申请日：2021-11-23
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
IPC: C01B3/52 , C01B3/56 , B01D53/047 , B01D53/12 , B01D53/14 , B01D53/18 , B01D53/32 , C01B3/24 , B01D5/00 , B01D47/10 , B01D17/02 , B01D29/27 , B01D29/66 , B01D46/00 , B01D53/04 , B01D53/48 , B01D53/76 , B01D61/36 , C01B3/38 , B01D50/60 , C01B3/58 , B01D53/26
CPC classification number: C01B3/52 , B01D5/006 , B01D5/009 , B01D5/0027 , B01D5/0072 , B01D5/0075 , B01D17/0208 , B01D29/27 , B01D29/66 , B01D46/0036 , B01D47/10 , B01D50/60 , B01D53/047 , B01D53/0423 , B01D53/0462 , B01D53/0476 , B01D53/12 , B01D53/1406 , B01D53/1412 , B01D53/1431 , B01D53/1462 , B01D53/1468 , B01D53/1487 , B01D53/18 , B01D53/265 , B01D53/326 , B01D53/48 , B01D53/76 , B01D61/362 , C01B3/24 , C01B3/38 , C01B3/382 , C01B3/386 , C01B3/56 , C01B3/58 , H05K999/99 , B01D2252/102 , B01D2252/103 , B01D2252/20436 , B01D2252/504 , B01D2252/602 , B01D2256/16 , B01D2256/20 , B01D2257/304 , B01D2257/306 , B01D2257/406 , B01D2257/504 , B01D2257/60 , B01D2257/708 , B01D2259/402 , C01B2203/025 , C01B2203/0227 , C01B2203/0233 , C01B2203/0261 , C01B2203/04 , C01B2203/042 , C01B2203/043 , C01B2203/045 , C01B2203/048 , C01B2203/0415 , C01B2203/0435 , C01B2203/0465 , C01B2203/0475 , C01B2203/0485 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/0877 , C01B2203/1235 , C01B2203/1241 , C01B2203/142 , C01B2203/147 , C01B2203/84 , Y02P20/129 , Y02P30/00
Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.
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17.发明公开公开(公告)号：US20230159837A1
公开(公告)日：2023-05-25
申请号：US18151095
申请日：2023-01-06
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Dave G. Newport , Daniel A. Burciaga , Daniel Michael Leo , Justin Kevin Miller , Brian Christopher Attwood
IPC: C10J3/84 , C07C41/01 , C07C29/151 , C10K3/06 , C10K1/00 , C10L1/02 , C10L1/06 , C10L1/08 , C10G2/00 , C01B3/34 , C01B3/50 , C12P7/06 , B01J19/24 , B01J19/00
CPC classification number: C10J3/84 , C07C41/01 , C07C29/1518 , C10K3/06 , C10K1/007 , C10K1/004 , C10L1/023 , C10L1/026 , C10L1/06 , C10L1/08 , C10G2/344 , C01B3/346 , C01B3/50 , C12P7/06 , B01J19/245 , B01J19/0013 , C10L2200/043 , C10L2270/04 , C10G2300/1051 , C10G2400/08 , C10L2200/0423 , C10L2270/023 , C10G2300/104 , C10G2400/02 , C10L2200/0446 , C10L2270/026 , C10G2300/1055 , C10G2400/04 , C10G2300/1022 , C10J2300/1823 , C10J2300/1853 , C10J2300/1884 , C10G2300/4081 , C10J2300/1656 , C10J2300/1665 , C10J2300/1659 , C10J2300/1671 , C10J2300/1643 , B01J2219/00157 , B01J2219/0004 , C01B2203/0233 , C01B2203/04 , C01B2203/062 , C01B2203/06 , C01B2203/84 , C01B2203/1235 , C01B2203/0822 , C10J2300/1628
Abstract: A method of producing liquid fuel and/or chemicals from a carbonaceous material entails combusting a conditioned syngas in pulse combustion heat exchangers of a steam reformer to help convert carbonaceous material into first reactor product gas which includes carbon monoxide, hydrogen, carbon dioxide and other gases. A portion of the first reactor product gas is transferred to a hydrogen reformer into which additional conditioned syngas is added and a reaction carried out to produce an improved syngas. The improved syngas is then subject to one or more gas clean-up steps to form a new conditioned syngas. A portion of the new conditioned syngas is recycled to be used as the conditioned syngas in the pulse combustion heat exchangers and in the hydrocarbon reformer. A system for carrying out the method include, a steam reformer, a hydrocarbon reformer, first and second gas-cleanup systems, a synthesis system and an upgrading system.
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公开(公告)号：US20220098036A1
公开(公告)日：2022-03-31
申请号：US17534251
申请日：2021-11-23
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
IPC: C01B3/52 , C01B3/56 , B01D53/047 , B01D53/12 , B01D53/14 , B01D53/18 , B01D53/32 , C01B3/24 , B01D5/00 , B01D47/10 , B01D17/02 , B01D29/27 , B01D29/66 , B01D46/00 , B01D50/00 , B01D53/04 , B01D53/48 , B01D53/76 , B01D61/36 , C01B3/38 , C01B3/58 , B01D53/26
Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.
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19.发明授权公开(公告)号：US10766059B2
公开(公告)日：2020-09-08
申请号：US16361817
申请日：2019-03-22
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Daniel A. Burciaga , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Justin Kevin Miller , Kaitlin Emily Harrington , Brian Christopher Attwood
IPC: B09B3/00 , C10J3/54 , C10J3/66 , C10J3/72 , C10J3/50 , C10B3/02 , C10B27/06 , C10B47/04 , C10B47/18 , C10B49/16 , C10B51/00 , C10B53/07 , C10J3/48
Abstract: A multi-stage product gas generation system converts a carbonaceous material, such as municipal solid waste, into a product gas which may subsequently be converted into a liquid fuel or other material. One or more reactors containing bed material may be used to conduct reactions to effect the conversions. Unreacted inert feedstock contaminants present in the carbonaceous material may be separated from bed material using a portion of the product gas. A heat transfer medium collecting heat from a reaction in one stage may be applied as a reactant input in another, earlier stage.
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公开(公告)号：US10350574B2
公开(公告)日：2019-07-16
申请号：US16126207
申请日：2018-09-10
Applicant: ThermoChem Recovery International, Inc.
Inventor： Ravi Chandran , Dave G. Newport , Daniel A. Burciaga , Daniel Michael Leo , Justin Kevin Miller , Kaitlin Emily Harrington , Brian Christopher Attwood
Abstract: A liquid fuel product system is configured to produce liquid fuels from carbonaceous materials. The liquid fuel product system includes a plurality of feedstock delivery systems, a plurality of first stage product gas generation systems, a plurality of second stage product gas generation systems, a plurality of third stage product gas generation systems, a primary gas clean-up system, a compression system, a secondary gas clean-up system, and a synthesis system that includes one or more from the group consisting of ethanol, mixed alcohols, methanol, dimethyl ether, and Fischer-Tropsch products.
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